Optimization of photo-hydrogen production based on cheese whey spent medium

Cheese whey wastewater diluted to 10 g lactose/L was initially subjected to dark-fermentation by Enterobacter aerogenes MTCC 2822, and the VFAs-rich spent medium (acetic acid 1900 mg/L, butyric acid 537 mg/L, and traces of propionic acid) was subjected to photo-fermentation through enrichment by Ni²⁺ (0–8 μmol/L), Fe²⁺ (0–100 μmol/L) or Mg²⁺ (0–15 mmol/L) in batch mode by Rhodopseudomonas BHU 01 strain. The maximum cumulative H₂ production (144 ml) and yield (58 mmol) was obtained at 4 μmol Ni²⁺/L. Likewise, Fe²⁺ (60 μmol/L) resulted in maximum cumulative H₂ production (139 ml) and yield (56 mmol). Nevertheless, 6 mmol of Mg²⁺ did not significantly affect H₂ production (110 ml) or yield (44 mmol); the latter value in close proximity with the control (37 mmol). The concomitant reduction in COD was maximum (15.61%) for 4 μmol Ni²⁺/L, followed by 15.33% for 60 μmol Fe²⁺/L, and the least for 6 mmol Mg²⁺/L (14.5%). The observations suggest the role of Fe²⁺ and Ni²⁺ in regulation of nitrogenase and hydrogenase, while that of Mg²⁺ mainly in the biosynthesis of photopigment bacteriochlorophyll (Bchl).     

Bio-hydrogen production and the F0F1-ATPase activity of Rhodobacter sphaeroides: Effects of various heavy metal ions

Rhodobacter sphaeroides MDC 6521 isolated from Arzni mineral springs in Armenia is able to produce bio-hydrogen (H₂) in anaerobic conditions upon illumination in the presence of various metal ions. The significant aspect in regulation of H₂ production by these bacteria and its energetics is the requirement for F₀F₁-ATPase, the main membrane enzyme responsible for generation of proton motive force under anaerobic conditions. In order to determine the mediatory role of F₀F₁ in H₂ production, the effects of various metal ions (Mn²⁺, Mg²⁺, Fe²⁺, Ni²⁺, and Mo⁶⁺) on N,N′-dicyclohexylcarbodiimide inhibited ATPase activity of R. sphaeroides membrane vesicles were investigated. These ions in appropriate concentrations considerably enhanced H₂ production, which was not observed in the absence of Fe²⁺, indicate the requirement for Fe²⁺. The R. sphaeroides membrane vesicles demonstrated significant ATPase activity. In the absence of Fe²⁺ inhibition (∼80%) of ATPase activity was observed, which was increased by addition of metal ions. A higher ATPase activity was detected in the presence of Fe²⁺ (80 μM) and Mo⁶⁺ (16 μM). These results indicate a relationship between the F₀F₁-ATPase activity and H₂ production that might be a significant pathway to provide novel evidence of a requirement for F₀F₁-ATPase in H₂ production by R. sphaeroides.     

Effects of Fe0 and Ni0 nanoparticles on hydrogen production from cotton stalk hydrolysate using Klebsiella sp. WL1316: Evaluation of size and concentration of the nanoparticles

Fe⁰ and Ni⁰ nanoparticles (NPs) of certain size were synthesized and added to the hydrogen production system from cotton stalk hydrolysate using Klebsiella sp. WL1316. Fe⁰ and Ni⁰ NPs with a size of 50 nm at all concentrations effectively improve hydrogen production during mid to late fermentation stages; particularly, the highest daily hydrogen production obtained following treatment with 50 nm Fe⁰ NPs at 30 mg/L fermented for 96 h significantly increased by 61% comparing to the control treatment. The reducing sugar consumption in cotton stalk hydrolysate and ΔOD₆₀₀ could be improved to some extent by Fe⁰ and Ni⁰ NPs supplementation. Addition of Fe⁰ or Ni⁰ NPs of 50 nm at a concentration of 30 mg/L resulted in enhanced cumulative hydrogen production with improvement of hydrogen yield reached higher than 20%, and the values of Y(H₂/S) were all higher than 90 mL/g _substrate, reflecting good hydrogen production and substrate consumption. The analysis of the main soluble metabolites profile revealed that supplementation with Fe⁰ and Ni⁰ NPs of suitable size and concentration may decrease the metabolic flux in the competitive branch of hydrogen production and increase the metabolic flux of the key node that leads to hydrogen generation, thus promoting biohydrogen synthesis.     

The effect of Ni,Fe and Mg concentration on photo-hydrogen production by Rhodopseudomonas faecalis RLD-53

In the present study, the effect of Ni²⁺ (0–10 μmol/l), Fe²⁺ (0–200 μmol/l) and Mg²⁺ (0–15 mmol/l) concentration on photo-hydrogen production from acetate was investigated by batch culture. Results showed that under a proper concentration range, Ni²⁺ was able to enhance the hydrogen production rate and the hydrogen yield; Fe²⁺ was able to increase the hydrogen yield, and hydrogen production rate was enhanced only when the culturing time was 24–72 h. Ni²⁺ and Fe²⁺ at a higher concentration inhibited cell growth. When Ni²⁺ and Fe²⁺ concentrations were 4 μmol/l and 80 μmol/l, respectively, maximal hydrogen yield of 2.87 and 2.78 mol H₂/mol acetate was obtained when batch culturing at 35 °C with initial pH 7.0. Mg²⁺ did not significantly affect hydrogen production and hydrogen yield which maintained at about 2.45 mol H₂/mol acetate, but it was favorable to cell growth.     

Effect of ferrous ion on photo heterotrophic hydrogen production by Rhodobacter sphaeroides

The effect of ferrous ion (0–3.2 mg/l) on photo heterotrophic hydrogen production was studied in batch culture using sodium lactate as substrate. The results showed that hydrogen production by Rhodobacter sphaeroides   was significantly suppressed when Fe²⁺${\mathrm{Fe}}^{2+}$ was limited. Hydrogen production increased linearly with an increase in Fe²⁺${\mathrm{Fe}}^{2+}$ concentration in the range of 0–1.6 mg/l; reaching a maximum at 2.4 mg/l. When hydrogen production was suppressed in the above medium, a pH increase to 8.9 was observed, and the ratio of lactate utilized to total organic carbon removal was found to be increased, indicating that more soluble organic products were produced. Under the Fe²⁺${\mathrm{Fe}}^{2+}$ limited conditions, ferrous iron was shown to have a greater effect on hydrogen production by Rb. sphaeroides than that by the anaerobic heterotrophic bacterium Clostridium butyricum.     

Methane free biohydrogen production from carbon monoxide using a continuously operated moving bed biofilm reactor

Biological water-gas shift (WGS) reaction is a green and sustainable alternative to thermochemical-catalytic WGS process for hydrogen production from carbon monoxide (CO). However, CO tolerant carboxydotrophic microbes for hydrogen production and scaling up the technology using a bioreactor system present challenges in successful application of this technology. This study demonstrated the capability of anaerobic microbial consortium for biohydrogen production from CO using a moving bed biofilm reactor (MBBR). The CO conversion pathway followed by the anaerobic biomass was first elucidated by inhibiting the methanogens present using 2-bromoethanesulfonate (BES) at an optimum concentration of 10 mmol/L. An increase in inlet CO concentration to the MBBR enhanced the H₂ production, but the CO conversion efficiency was low. More than 80% CO conversion efficiency was obtained only for a low inlet CO concentration. A maximum H₂ concentration of 19.5 mmol/L along with 2 mmol/L of acetate were obtained for 36 mmol/L of inlet CO concentration in the bioreactor. The carbon flux analysis showed that the CO was mainly utilized for methane free H₂ production, and only <10% of carbon flux was diverted towards acetate formation. Overall, this study demonstrated that MBBR system can be used for steady state biohydrogen production over a prolonged operation period.     

Ni (II) and Mg (II) ions as factors enhancing biohydrogen production by Rhodobacter sphaeroides from mineral springs

Various metal ions play a key role in biohydrogen (H₂) production by phototrophic bacteria through incorporation into or stimulating the responsible enzymes and/or related pathways. The Ni (II) and Mg (II) ions effects on growth and H₂ production by Rhodobacter sphaeroides strain MDC6521 isolated from mineral springs in Armenia were established. The highest growth specific rate was obtained with 4–6 μM Ni²⁺ and 5 mM Mg²⁺. pH of the growth medium changed from 7.0 to 9.2–9.4 during the bacterial growth up to 72 h in spite of Ni²⁺ added but pH increased in different manner with Mg²⁺. In the presence of 2–4 μM Ni²⁺ external oxidation-reduction potential (ORP) decreased to more negative values (−800 ± 15 mV). This decrease of ORP indicated ∼2.7-fold enhanced H₂ yield (9.80 mmol L⁻¹) with Ni²⁺ compared with the control (without Ni²⁺). The H₂ yield determined in the medium with Mg²⁺ was ∼2.2 fold higher than that with 1 mM Mg²⁺. These results reveal new regulatory ways to improve H₂ production by R. sphaeroides those were depending on Ni²⁺ and Mg²⁺ of different concentrations.     

Simultaneous thermophilic hydrogen production and phenol removal from palm oil mill effluent by Thermoanaerobacterium-rich sludge

Thermoanaerobacterium-rich sludge was used for hydrogen production and phenol removal from palm oil mill effluent (POME) in the presence of phenol concentration of 100–1000 mg/L. Thermoanaerobacterium-rich sludge yielded the most hydrogen of 4.2 L H₂/L-POME with 65% phenol removal efficiency at 400 mg/L phenol. Butyric acid and acetic acid were the main metabolites. The effects of oil palm ash, NH₄NO₃ and iron concentration (Fe²⁺) on hydrogen production and phenol removal efficiency from POME by Thermoanaerobacterium-rich sludge was investigated using response surface methodology (RSM). The RSM results indicated that the presence of 0.2 g Fe²⁺/L, 0.3 g/L NH₄NO₃ and 20 g/L oil palm ash in POME could improved phenol removal efficiency, with predicted hydrogen production and phenol removal efficiency of 3.45 L H₂/L-POME and 93%, respectively. In a confirmation experiment under optimized conditions highly reproducible results were obtained, with hydrogen production and phenol removal efficiency of 3.43 ± 0.12 L H₂/L-POME and 92 ± 1.5%, respectively. Simultaneous hydrogen production and phenol removal efficiency in continuous stirred tank reactor at hydraulic retention time (HRT) of 1 and 2 days were 4.0 L H₂/L-POME with 85% and 4.2 L H₂/L-POME with 92%, respectively. Phenol degrading Thermoanaerobacterium-rich sludge comprised of Thermoanaerobacterium thermosaccharolyticum, Thermoanaerobacterium aciditolerans, Desulfotomaculum sp., Bacillus coagulans and Clostridium uzonii. Phenol degrading Thermoanaerobacterium-rich sludge has great potential to harvest hydrogen from phenol-containing wastewater.     

Magnetite nanoparticles enhanced glucose anaerobic fermentation for bio-hydrogen production using an expanded granular sludge bed (EGSB) reactor

The feasibility and efficiency of magnetite nanoparticles (Fe₃O₄NPs) enhanced bio-hydrogen production from glucose anaerobic fermentation were evaluated in this study. The results demonstrated that the maximum hydrogen yield (HY) of 12.97 mL H₂/g-VSS was obtained with 50 mg/L and 40–60 nm of Fe₃O₄NPs in batch experiments. Moreover, the optimum dosage of Fe₃O₄NPs produced hydrogen production (HP) of 4.95 L H₂/d in an expanded granular sludge bed (EGSB) reactor. Fe₃O₄NPs involved could promote ethanol and acetic acid accumulation. Fe²⁺ as by-product of iron corrosion could effectively promote the activity of key coenzymes and soluble microbial products (SMPs). Importantly, Fe₃O₄NPs addition resulted in the formation of electronic conductor chains to enhance the electron transport efficiency in the granular sludge. Microbial community analysis revealed that the relative abundance of butyrate-hydrogen-producing bacteria (Clostridium) decreased from 40.55% to 11.45%, while the relative abundance of ethanol-hydrogen-producing bacteria (Acetanaerobacterium and Ethanoligenens) increased from 19.62% to 35.35% with Fe₃O₄NPs involved, confirming that the fermentation type was transformed from butyrate-type to ethanol-type, which finally facilitated more hydrogen production.     

Effect of Ni2+ concentration on fermentative hydrogen production using waste activated sludge as substrate

The influence of Ni²⁺ concentration on biohydrogen production was investigated using waste activated sludge as substrate. The degradation of substrate, accumulation of volatile fatty acids (VFAs) and distribution of microbial community were analyzed to provide information for influencing mechanisms of Ni²⁺ addition. The experimental results demonstrated that the efficiency of hydrogen fermentation from waste activated sludge could be significantly improved. The optimal Ni²⁺ concentration was 5 mg/L, and under this concentration, the cumulative hydrogen production was 1.29 times of the control group. The degradation of soluble chemical oxygen demand (SCOD) increased from 25.21% to 27.69% when the added Ni²⁺ concentration was 5 mg/L. The analysis of microbial community distribution revealed that Ni²⁺ decreased the microbial diversity, and provided more suitable condition for the microbial growth and activity of hydrogen-producers. Citrobacter was the dominant hydrogen-producers in the control group, they changed into Enterococcus when 5 mg/L Ni²⁺ was added. Besides, the proportion of Clostridium_sensu_stricto_1, which is regarded as the primary hydrogen-producing bacteria under numerous operating conditions, was also significantly increased in the presence of Ni²⁺.     

Microbial culture selection for bio-hydrogen production from waste ground wheat by dark fermentation

Hydrogen formation performances of different anaerobic bacteria were investigated in batch dark fermentation of waste wheat powder solution (WPS). Serum bottles containing wheat powder were inoculated with pure cultures of Clostridium acetobutylicum (CAB), Clostridium butyricum (CB), Enterobacter aerogenes (EA), heat-treated anaerobic sludge (ANS) and a mixture of those cultures (MIX). Cumulative hydrogen formation (CHF), hydrogen yield (HY) and specific hydrogen production rate (SHPR) were determined for every culture. The heat-treated anaerobic sludge was found to be the most effective culture with a cumulative hydrogen formation of 560 ml, hydrogen yield of 223 ml H₂ g⁻¹ starch and a specific hydrogen production rate of 32.1 ml H₂ g⁻¹ h⁻¹.     

Firmicutes with iron dependent hydrogenase drive hydrogen production in anaerobic bioreactor using distillery wastewater

Distillery wastewater rich in organics is an inexpensive renewable resource for making first generation biofuel. Distillery wastewaters are mostly treated via the biomethanation route; however, in this study the conditions in sequential batch reactor (SBR) are being set to develop and analyze the microbial community that opted for hydrogen production. An optimum performance condition for a bioreactor was achieved after 40 days of operation, which gave substrate degradation rate of 0.72 kg/m³-day with volumetric hydrogen production of 0.32 mol H₂/m³-day. Study proposes that the dominant Delftia sp., a hydrogen oxidizing bacterium has been replaced during hydrogen production mode with dominant Anaerofilum sp., an anaerobic Firmicute and the iron dependent hydrogenases dominated as functional gene for hydrogen production. Future studies are required where process-engineering interventions could be applied to improve the hydrogen driving biochemical process.     

Enhancement of hydrogen production by the filamentous non-heterocystous cyanobacterium Arthrospira sp. PCC 8005

The efficiency of hydrogen production by different cyanobacterial species depends on several external factors. We report here the factors enhancing hydrogen production by filamentous non-heterocystous cyanobacterium Arthrospira sp. PCC 8005. Cells adapted to dark-anaerobic conditions produced hydrogen consistent with increased hydrogenase activity when supplemented with Fe²⁺. Stimulation of hydrogen production could be achieved by addition of reductants, either dithiothreitol or β-mercaptoethanol with higher production observed with the latter. Additionally, Fe²⁺ and β-mercaptoethanol added to nitrogen- and sulphur-deprived cells significantly stimulated H₂ production with maximal value of 5.91 ± 0.14 μmol H₂ mg Chla⁻¹ h⁻¹. Glucose and a small increase of osmolality imposed by either NaCl or sorbitol enhanced hydrogen production. High rates of hydrogen production were obtained in cells adapted in nitrogen-deprived medium with neutral and alkaline external pH, significant decrease of hydrogen production occurred under acidic external pH.     

Co-fermentation of sewage sludge and algae and Fe2+ addition for enhancing hydrogen production

Co-fermentation of sewage sludge and algae was performed for enhancing the hydrogen production, and the effect of Fe²⁺ on co-fermentation process was examined. Results showed that both co-fermentation process and Fe²⁺ addition promoted hydrogen production. Highest hydrogen production of 28 mL/100 mL (14.8 mL H₂/g VS_added) was obtained from the co-fermentation group with 600 mg/L Fe²⁺ addition, which was 2.15 times, 2.00 times and 1.87 times of mono-fermentation of sludge, mono-fermentation of algae, and the co-fermentation group without Fe²⁺ addition. Both volatile solids and protein degradation were stimulated by co-fermentation process. Microbial analysis showed that co-fermentation groups with Fe²⁺ addition enriched Clostridium sensu stricto 13, Clostridium tertium and Terrisporobacter, which were positively correlated with cumulative hydrogen production. This study suggested that the co-fermentation of sludge and algae in the presence of Fe²⁺ could significantly improve the hydrogen production by stimulating the hydrogen-producing metabolism.     

Production,characterization of acetyl esterase from a rumen bacteria strain RB3, and application potential of the strain in biodegradation of crop residues

Acetyl esterase was produced by a bacterial strain RB₃ at a level of 0.59 U mL⁻¹. The strain was isolated from beef cattle rumen fluid under anaerobic condition, and was identified as Escherichia coli. The peak activity of the enzyme appeared after 48 h of culturing under anaerobic condition. The optimal pH of the enzyme activity was 8.0, and the optimal temperature was 40 °C. The K_m and V_max values on p-nitrophenyl acetate were 0.84 mM and 0.13 mmol p-nitrophenol liberated min⁻¹ mg of protein⁻¹ respectively. The enzyme activity could be promoted by Zn²⁺, Ni²⁺, Fe²⁺, and K⁺, and inhibited by Cu²⁺, Fe³⁺, Mn²⁺, Mg²⁺, Ca²⁺, and Co²⁺. Biodegradation of rice stalk and maize stover by the strain RB3 and Pleurotus ostreatus was compared. The strain showed higher degradation rate for hemicellulose in the crop residues, while P. ostreatus showed higher degradation rate for cellulose. This indicated the potential industrial application of the strain RB3, particularly in utilizing renewable lignocellulose containing acetyl xylan for fermentation of products.     

Water enhanced methanol decomposition for simultaneous heat recovery and ready-to-use synthesis gas production over CO2 capture enhanced Ni/zeolite 4A catalyst

Methanol decomposition is considered as a “one stone two birds” approach for simultaneously recovering waste heat and affording synthesis gas. However, this approach requires efficient catalysts with high CO selectivity and low selectivity to byproducts. Herein, a rational design of CO₂ capture enhanced Ni/zeolite 4 A catalyst for synthesis gas production by water enhanced methanol decomposition is reported. 5%-Ni/NaA-500 catalyst achieves the Y_H2 of 80.6%, Y_CO of 76.2%, H₂/CO molar ratio of 2.11, high stability, low selectivity to CO₂ and CH₄, and no coke at 325 °C. Ni atoms highly disperse on the surface and microporous of zeolite 4 A, and the strong interaction between Ni atoms and zeolite 4 A inhibits the reduction of Ni atoms. Consequently, Ni³⁺, Ni²⁺ and Ni⁰ coexist in 5%-Ni/NaA-500, and the redox couples of Ni³⁺↔Ni²⁺, Ni²⁺↔Ni⁰, and Ni³⁺↔Ni⁰ will enhance the redox processes during methanol decomposition. CO₂ capture capacity of x%-Ni/NaA-Y below 350 °C promotes the reverse water gas shift reaction by concentrating CO₂ molecules, which hence increases CO selectivity and declines the selectivity to byproducts. The reaction path follows CH₃OH→CH₃O→CH₂O→CHO→CO. This work will pave the way to industrial applications that combine ready-to-use synthesis gas production and heat recovery.     

Catalytic partial oxidation of n-butanol for hydrogen production over LDH-derived Ni-based catalysts

Catalytic partial oxidation (CPOX) of n-butanol is an alternative route for hydrogen production from bio-mass. An analysis on the thermodynamics using Gibbs free energy minimization method was carried out, and the results indicated that a higher H₂ yield can be obtained near 700 °C or above with O₂/butanol = 1.5–2.0. Layered double hydroxide (LDH) derived catalysts were proved effective in CPOX, and the Ni_0.35Mg_2.65Al_0.5Fe_0.5O_4.5±δ catalyst produced about 4.03 mol-H₂/mol-butanol at 700 °C with a feed of O₂/butanol = 2.0. This higher activity can be attributed to the structural and electronic properties: there is a higher surface area of 178.2 m²/g, and more Ni⁰ atoms were obtained and remained stable in the 31-h CPOX test.     

Impact of regulated pH on proto scale hydrogen production from xylose by an alkaline tolerant novel bacterial strain, Enterobacter cloacae DT-1

A hydrogen producing facultative anaerobic alkaline tolerant novel bacterial strain was isolated from crude oil contaminated soil and identified as Enterobacter cloacae DT-1 based on 16S rRNA gene sequence analysis. DT-1 strain could utilize various carbon sources; glycerol, CMCellulose, glucose and xylose, which demonstrates that DT-1 has potential for hydrogen generation from renewable wastes. Batch fermentative studies were carried out for optimization of pH and Fe²⁺ concentration. DT-1 could generate hydrogen at wide range of pH (5–10) at 37 °C. Optimum pH was; 8, at which maximum hydrogen was obtained from glucose (32 mmol/L), when used as substrate in BSH medium containing 5 mg/L Fe²⁺ ion. Decrease in hydrogen partial pressure by lowering the total pressure in the fermenter head space, enhanced the hydrogen production performance of DT-1 from 32 mmol H₂/L to 42 mmol H₂/L from glucose and from 19 mmol H₂/L to 33 mmol H₂/L from xylose. Hydrogen yield efficiency (HY) of DT-1 from glucose and xylose was 1.4 mol H₂/mol glucose and 2.2 mol H₂/mol xylose, respectively. Scale up of batch fermentative hydrogen production in proto scale (20 L working volume) at regulated pH, enhanced the HY efficiency of DT-1 from 2.2 to 2.8 mol H₂/mol xylose (1.27 fold increase in HY from laboratory scale). 84% of maximum theoretical possible HY efficiency from xylose was achieved by DT-1. Acetate and ethanol were the major metabolites generated during hydrogen production.